Manufacturing Process for Polysaccharide Beads

ABSTRACT

The invention discloses a method of manufacturing polysaccharide beads, comprising the steps of: i) providing a water phase comprising an aqueous solution of a polysaccharide; ii) providing an oil phase comprising at least one water-immiscible organic solvent and at least one oil-soluble emulsifier; iii) emulsifying the water phase in the oil phase to form a water-in-oil (w/o) emulsion; and iv) inducing solidification of the water phase in the w/o emulsion, wherein the organic solvent is an aliphatic or alicyclic ketone or ether.

TECHNICAL FIELD OF THE INVENTION

The present invention relates to polysaccharide beads, and moreparticularly to manufacture of polysaccharide beads by inversesuspension techniques. The invention also relates to crosslinkedpolysaccharide beads and to use of the beads for separation purposes.

BACKGROUND OF THE INVENTION

Crosslinked polysaccharide beads are commonly used as stationary phasesfor chromatographic separation of proteins and other biomolecules. Suchbeads were introduced in the early 1960-ies (see e.g. U.S. Pat. No.3,208,994, which is hereby incorporated by reference in its entirety),mainly for laboratory separation purposes. Since then their use hasgrown dramatically and crosslinked polysaccharide beads are now usedroutinely in large scale manufacturing processes for separation of manybiopharmaceuticals such as monoclonal antibodies, plasma components,insulin and various recombinant proteins.

The most common way to prepare polysaccharide beads is by inversesuspension processes, where an aqueous solution of a polysaccharide isemulsified as a water-in-oil (w/o) emulsion in a continuous oil phaseand the emulsion droplets are solidified either by crosslinking or bythermal gelation. Such processes are described in e.g. U.S. Pat. Nos.3,208,994, 4,794,177 and 6,602,990 (hereby incorporated by reference intheir entireties), which use chlorinated hydrocarbons or aromatichydrocarbons as the oil phase. An issue here is that large scale use ofhalogenated hydrocarbons and aromatic hydrocarbons is currently beingphased out for environmental reasons.

Accordingly there is a need for methods to manufacture polysaccharidebeads without the use of halogenated or aromatic solvents.

SUMMARY OF THE INVENTION

One aspect of the invention is to provide an environmentally acceptablemethod of manufacturing polysaccharide beads. This is achieved with amethod as defined in the claims.

One advantage is that the method does not use halogenated or aromaticsolvents. Further advantages are that spherical beads with good porestructures and mechanical properties can be obtained.

A second aspect of the invention is to provide a polysaccharide beadsuitable for separation purposes. This is achieved with a bead asdefined in the claims.

A third aspect of the invention is to provide a use for separationpurposes of the crosslinked beads. This is achieved with a use asdefined in the claims.

Further suitable embodiments of the invention are described in thedependent claims.

DRAWINGS

FIG. 1 shows an outline of the method of the invention. a) addition ofthe water phase to the oil phase, b) water-in-oil emulsion, c)solidified beads dispersed in oil phase.

FIG. 2 shows the crosslinking of dextran with epichlorohydrin accordingto an embodiment of the invention.

FIG. 3 shows microscope pictures of the swollen particles from a) sample9090 (2-MCH) and b) sample 5595 (3-MCH).

FIG. 4 shows microscope pictures of the swollen particles from sample5624 (cyclohexane+3-MCH).

FIG. 5 shows microscope pictures of the swollen particles from a) sample6462 (CPME) and b) sample 5182 (CPME+3-MCH).

FIG. 6 shows microscope pictures of the swollen particles from a) sample6671 (DIBK) and b) sample 5382 (DIBK+3-MCH).

FIG. 7 shows microscope pictures of the swollen particles from sample9355 (MAK).

DETAILED DESCRIPTION OF EMBODIMENTS

In one aspect, illustrated by FIGS. 1-2, the present invention disclosesa method of manufacturing polysaccharide beads, comprising the steps of:

i) Providing a water phase 1 comprising an aqueous solution of apolysaccharide. This can be accomplished by dissolving a polysaccharidein water or in water comprising one or more additional components suchas salts, buffers, alkali, reducing agents etc. The polysaccharide cane.g. be a native polysaccharide such as dextran, pullulan, starch,alginate, guar gum, locust bean gum, konjac, agar, agarose, carrageenanetc. As an example, the polysaccharide can be dextran, e.g. dextran witha weight average molecular weight, Mw, of 20-4000 kDa, 40-2000 kDa or100-500 kDa. Alternatively, the polysaccharide can be a derivative of anative polysaccharide, such as a cellulose ether, an agarose ether, astarch ether, DEAE dextran etc. Advantageously, the polysaccharide iswater-soluble at room temperature or at elevated temperatures.

ii) Providing an oil phase 2 comprising at least one water-immiscibleorganic solvent and at least one oil-soluble emulsifier. Thewater-immiscible organic solvent(s) can suitably have a water solubilityof less than 5 vol. %, such as less than 3 vol. % or less than 2 vol. %at 25° C. and the solubility of water in the water-immiscible organicsolvent(s) can suitably be less than 5 vol. %, such as less than 3 vol.% or less than 2 vol. % at 25° C. The oil-soluble emulsifier(s) cansuitably be soluble in the organic solvent(s) and the oil phase can beprepared by dissolving one or more oil-soluble emulsifiers in thewater-immiscible organic solvent or a mixture of water-immiscibleorganic solvents. The concentration of the emulsifier in the oil phasecan e.g. be 0.01-0.5 g/ml, such as 0.05-0.3 g/ml. These values can alsorefer to the total concentration of emulsifiers in the oil phase, incase mixed emulsifiers are used. If a polymeric emulsifier is used, theviscosity of the oil phase may vary with the molecular weight andconcentration of the emulsifier.

-   iii) Emulsifying the water phase in the oil phase to form a    water-in-oil (w/o) emulsion. As illustrated in FIG. 1, this can e.g.    be done by adding the water phase 1 to the oil phase 2 in an    emulsification vessel 3 under agitation provided by an agitator 4,    such that the water phase is dispersed as discrete liquid droplets 5    in the continuous oil phase 2, stabilized by the emulsifier. Other    techniques known in the art can also be used, e.g. continuous    emulsification using static mixers, membrane emulsification etc.    Depending on the viscosity of the oil phase, some optimization of    the agitation intensity may be required to achieve specific particle    sizes of the beads produced. Alternatively (or additionally), the    concentration and/or type of the emulsifier may be varied in order    to get certain particle sizes.

iv) Inducing solidification of the water phase in the w/o emulsion. Thismeans that the liquid droplets 5 are converted to (solid) gel beads 6 bygelation of the polysaccharide. The gelation can be induced e.g. byadding a crosslinking agent to chemically (covalently) crosslink thepolysaccharide, as further discussed below, or by lowering thetemperature to cause thermal gelation of the polysaccharide, as is alsodiscussed below. Once the water phase droplets have been solidified intogel beads, the beads may be recovered by sedimentation and/or filtrationand they may be further washed and processed to provide beads suitablefor separation or cell cultivation purposes. The further processing maye.g. include further crosslinking steps and/or derivatisation withreagents to introduce functional groups.

The at least one organic solvent is an aliphatic or alicyclic ketone orether. Alternatively, or additionally, the at least one organic solventdoes not contain halogens (i.e. the molecules of the solvent do notcontain halogen atoms) and has Hansen solubility parameter values in theranges of βD=15.0-18.5 MPa^(1/2), βP=3.5-8.5 MPa^(1/2) and δH=4.0-5.5MPa^(1/2). The oil phase can also comprise a mixture of halogen-freewater-immiscible organic solvents, where the mixture has Hansensolubility parameter values in the ranges of δD=15.0-18.5 MPa^(1/2),δP=3.5-8.5 MPa^(1/2) and δH=4.0-5.5 MPa^(1/2). Suitably, the content ofhalogenated solvents in the oil phase can be less than 1 mol %, such asless than 0.1% or less than 0.01%. The Hansen solubility parameters arediscussed in detail in C M Hansen: The three dimensional solubilityparameter and solvent diffusion coefficient—Their importance in surfacecoating formulation, Copenhagen 1967. δD is the dispersion forcecontribution to the solubility parameter (cohesive energy density) of asolvent, while δP is the polar force contribution and δH is the hydrogenbonding force contribution. Tables of Hansen solubility parameters fordifferent solvents can be found e.g. in J Brandrup, E H Immergut Eds.Polymer Handbook, 3^(rd) edition, John Wiley & Sons 1989, pp.VII/540-VII/544.

In certain embodiments, illustrated by FIG. 2, step iv) comprisescrosslinking the polysaccharide. This can be accomplished e.g. by addinga crosslinking agent to the w/o emulsion. The crosslinking agent maye.g. be a compound with two electrophilic functionalities, which canreact e.g. with two hydroxyl groups on the polysaccharide and causecrosslinking by the formation of covalently bonded links betweenpolysaccharide chains. The hydroxyl groups are particularly nucleophilicat high pH conditions and it can be advantageous to use a high pH waterphase in the method, e.g. by adding NaOH or other suitable alkali (e.g.KOH) to the water phase. The alkali (NaOH or KOH) concentration in thewater phase may e.g. be at least 0.1 M, such as 0.1-2 M or 0.5-1 M.Examples of electrophilic crosslinkers include epichlorohydrin,diepoxides and multifunctional epoxides, as well as divinylsulfone andhalohydrins like 1,3-dibromo-propanol-2. The crosslinker can suitably beadded to the w/o emulsion, such that it dissolves in the oil phase anddiffuses into the water phase droplets.

In some embodiments, step iv) comprises thermal gelation of thepolysaccharide. In this case, the polysaccharide can be a hot-watersoluble polysaccharide that forms a gel upon cooling. Examples of suchpolysaccharides are e.g. agar and agarose, which are soluble attemperatures of about 60° C. and higher but form solid gels upon coolingto e.g. about 40° C. or lower. In this case, steps i)-iii) can beperformed at a temperature where the polysaccharide is soluble and instep iv) the temperature is lowered to a temperature below the gel pointof the particular polysaccharide used.

In certain embodiments, at least one emulsifier is a cellulosederivative, such as a cellulose ester or a cellulose ether. Amongcellulose esters, cellulose mixed esters, such as cellulose acetatebutyrate can be particularly useful. Cellulose acetate butyrate (CAB) ofdifferent grades is commercially available, e.g. from Eastman ChemicalCompany (USA). The molecular weight of the CAB can suitably be 10-100kDa, such as 15-75 kDa or 16-70 kDa, determined by gel permeationchromatography as the polystyrene equivalent number average molecularweight (Mn). The acetyl and butyryl contents can e.g. be 2-20 wt. %acetyl content and 20-60 wt. % butyryl content, such as a) 10-15 wt. %acetyl content and 30-40 wt. % butyryl content orb) 2-5 wt. % acetylcontent and 50-60 wt. % butyryl content or c) 2-15 wt. % acetyl contentand 30-60 wt. % butyryl content. An example of a cellulose ether usefulas an emulsifier is ethyl cellulose.

In some embodiments at least one organic solvent is a C₆-C₁₀ aliphaticor alicyclic ketone or ether, such as a C₆-C₁₀ alicyclic ketone orether. Examples of such solvents are those defined by Formula I, II orIII,

wherein:

R₁ and R₂ are, independently of each other, C₁-C₅ alkyl groups;

R₃ is a C₁-C₅ alkylene group;

R₄ is hydrogen or a C₁-C₅ alkyl group attached to any one of thenon-carbonyl carbon atoms in the ring structure; and

R₅ and R₆ are, independently of each other, C₁-C₆ alkyl or cycloalkylgroups.

In some embodiments, at least one organic solvent is defined by FormulaII, with R₃ and R₄ defined as above. R₃ may e.g. be a C₂ alkylene groupand R₄ may be a methyl group.

In certain embodiments, the organic solvent can be selected from thegroup consisting of 2-methylcyclohexanone, 3-methylcyclohexanone,4-methylcyclohexanone, cyclohexanone, diisobutyl ketone, methyl n-amylketone, methyl isoamyl ketone, methyl isobutyl ketone, cyclopentylmethyl ether and their mixtures. At least one organic solvent can e.g.be selected from the group consisting of 2-methylcyclohexanone,3-methylcyclohexanone, 4-methylcyclohexanone, cyclohexanone, methyln-amyl ketone, methyl isoamyl ketone, methyl isobutyl ketone andcyclopentyl methyl ether, such as from the group consisting of2-methylcyclohexanone, 3-methylcyclohexanone, 4-methylcyclohexanone andcyclohexanone. In specific cases at least one organic solvent can be2-methylcyclohexanone.

In a second aspect the invention discloses a polysaccharide bead, or aplurality of polysaccharide beads, prepared by the method of anyembodiment disclosed above. The invention also discloses a crosslinkedpolysaccharide bead, or a plurality of crosslinked polysaccharide beads,comprising at least 0.1 ppm, such as 0.1-100 ppm of a C₆-C₁₀ aliphaticor alicyclic ketone or ether. This may e.g. constitute solvent residuesfrom a manufacturing process as discussed above. The amount may bemeasured e.g. by headspace GC or GC analysis of extracts, using e.g.mass spectroscopy or flame ionization as detection method. The C₆-C₁₀aliphatic or alicyclic ketone or ether can be as defined by Formulas I,II or III as discussed above and it can e.g. be selected from the groupconsisting of 2-methylcyclohexanone, 3-methylcyclohexanone,4-methylcyclohexanone, cyclohexanone, diisobutylketone, methyln-amylketone, methyl isoamyl ketone, methyl isobutyl ketone, cyclopentylmethyl ether and their mixtures.

In some embodiments, the bead or plurality of beads have a diameter of40-125 μm in dry form. In the case of a plurality of beads, the diametercan be determined as the volume-weighted median diameter, d50v, e.g. bylaser light diffraction or by electrozone sensing counting techniques.

In certain embodiments, the bead or plurality of beads comprise at least0.1 mmol/g, or 1-6 mmol/g, covalently bonded charged groups, such ascarboxymethyl-, sulfopropyl-, diethyl aminoethyl-, and/ordiethyl-(2-hydroxy-propyl)aminoethyl-groups. Such groups are useful forion exchange separations and groups like diethyl aminoethyl groups canalso promote the growth of adherent cells when the beads are used asmicrocarriers in cell cultivation. The derivatisation with chargedgroups can be accomplished by methods well known in the art.

In a third aspect, the invention discloses the use of one or morepolysaccharide beads as described above for separation of a targetbiomolecule, such as a target protein, from impurities or contaminants.

In a fourth aspect, the invention discloses the use of one or morepolysaccharide beads as described above as microcarriers for cultivationof cells.

EXAMPLES

Emulsification method (reference example with 1,2-dichloroethane) 165 gdextran of Mw 150-250 kD was dissolved in 390 ml distilled water andsimultaneously 22 ml 50% sodium hydroxide (NaOH) was added understirring. 0.8 g sodium borohydride (NaBH₄) was added to the solution.

21g cellulose acetate butyrate (CAB) was added into a 1000 ml glassreactor with an overhead agitator. The agitator was started and 350 ml1,2-dichloroethane (EDC) was added (the CAB concentration was thus 0.060g/ml EDC). The solution was stirred until the CAB had dissolved. Thewater phase was then added to the oil phase under agitation at 50° C.and the agitation was continued until a suitable droplet size had beenreached, as judged from microscopy of small samples withdrawn. When asuitable size was obtained, the emulsion was immediately stabilised byadding 22.4 ml epichlorohydrin (ECH) to crosslink the dextran and thussolidifying the droplets. 20 minutes after the addition of ECH, 50 ml ofEDC was added to make the reaction mixture less viscous and easier toagitate.

The crosslinking reaction was terminated after 20±4 h by adding 500 mlacetone. The reaction mixture was then transferred to a 3000 ml glassreactor containing 1250 ml acetone. The solution was stirred for 30 minand then the gel was subsequently allowed to sediment. The supernatantwas decanted and the washing procedure was repeated 5 times with acetoneand then 7 times with 60% aqueous ethanol and 4 times with 95% ethanol.The gel was then dried under vacuum at 60° C. for 48 h and the resultingpowder was sieved between 40 and 100 μm sieves.

The results from five repetitions of this experiment are shown in Table2, as samples 3077, 3088, 3092, 3081 and 1175.

SEC Analysis

Approximately 3-4 grams of powder was weighed in a plastic bottle towhich roughly 100 ml of either a 9 mg/ml NaCl solution or the runningbuffer (0.15M NaCl+0.05 M phosphate buffer, pH 7.0) was added. The gelwas left to swell and sediment for at least 16 hours. It was then washedseveral times and diluted in the running buffer to generate a 50-60% gelslurry. Columns of 10 mm diameter and 30 cm height (GE HealthcareHR10/30) were packed with the initial flow rate of either 1.0 or 1.2ml/min, and the final flow rate was either 1.2 or 1.7 ml/min. The packedcolumns were then tested in an effectiveness test and evaluated throughselectivity tests with dextran standards and proteins as described in LHagel: pp. 51-87 in J C Janson (Ed): Protein Purification: Principles,High Resolution Methods, and Applications, 3^(rd) edition, Wiley 2011.The test proteins were alpha chymotrypsinogen type II, bovine (Mw 26kDa), ribonuclease A, bovine (Mw 13.7 kDa) and lysozyme, chicken (Mw14.3 kDa), with 0.15 M NaCl, 0.05M Sodium Phosphate, pH 7.0 as runningbuffer. K_(D) data (i.e. the fraction of the bead volume accessible fora probe molecule of a particular size) for these proteins on theprototypes are shown in Table 3.

Water Regain

Water regain (Wr) is the amount of water taken up inside the beads for 1g dry beads. A high Wr value indicates that the swollen gel is lessdense and can separate high Mw target molecules.

15 g of dry beads were equilibrated with 500 ml water for 24 h. A3.3×11.5 cm weighed centrifuge tube with a 10 μm bottom filter wasfilled with the gel slurry and centrifuged at 1800 rpm for 10 min. Afterdetermining the wet weight of the tube, it was dried over night at 105°C. and the dry weight was determined. The water regain was calculated asthe drying weight loss (as ml water) per g dry gel.

Particle Size Distribution

The particle size distribution was measured in a Coulter Multisizer(Beckman Coulter), using the electrozone sensing technique.

Microscopic Examination

After crosslinking, the beads were examined in a light microscope withphase contrast optics and the presence of surface dimples, inclusions,aggregates etc. was noted.

Emulsifications with Different Solvents

Solvent Abbreviations

CPME—Cyclopentyl methyl ether

DIBK—Diisobutyl ketone (2,6-dimethyl-4-heptanone)

EDC—1,2-dichloroethane

MAK—Methyl n-amyl ketone

2-MCH—2-methylcyclohexanone

3-MCH—3-methylcyclohexanone

4-MCH—4-methylcyclohexanone

Emulsifications were carried out according to the reference exampleabove, with other solvents replacing EDC, and in some cases withdifferent types and/or concentrations of CAB. The CAB types used arespecified in Table 1. The beads were characterized as described aboveand the results are collated in Tables 2 and 3 and in the discussionbelow.

TABLE 1 CAB types used (all from Eastman Chemical Company and with dataaccording to the supplier's data sheets) Molecular Butyryl Acetyl CABweight*, Viscosity**, content, content, type kDa poise wt % wt % 381-0.5  30 1.9 37 13 381-20  70 76 37 13.5 500-5  57 19 51 4  551-0.0116 0.038 53 2 *Polystyrene equivalent number average molecular weight(Mn), as determined by gel permeation chromatography **Viscositydetermined by ASTM Method D 1343. Results converted to poises (ASTMMethod D 1343) using the solution density for Formula A as stated inASTM Method D 817 (20% Cellulose ester, 72% acetone, 8% ethyl alcohol).

TABLE 2 Results from emulsifications with different solvents and solventcombinations CAB CAB conc. Wr d50v Sample Solvent 1 Solvent 2 type g/ml(ml/g) (μm) 3077 EDC — 381-20   0.060 4.93 70.5 3088 EDC — 381-20  0.060 5.03 67.8 3092 EDC — 381-20   0.060 4.96 70.7 3081 EDC — 381-20  0.060 5.06 72.0 1175 EDC — 381-20   0.060 4.90 70.9 9090 2-MCH —381-20   0.060 4.74 33.1 5133 3-MCH — 381-20   0.060 4.77 42.4 55053-MCH — 381-20   0.054 4.60 50.7 5595 3-MCH — 381-0.5  0.060 4.94 72.75892 3-MCH — 381-0.5  0.090 5.17 73.6 5928 3-MCH — 500-5   0.060 5.0757.0 4904 4-MCH — 381-20   0.060 4.62 44.5 5624 Cyclo- 3-MCH 381-20  0.060 4.71 42.3 hexane (80 vol %) (20 vol %) 5806 Cyclo- 3-MCH 551-0.010.21 5.15 68.9 hexane (25 vol %) (75 vol %) 6462 CPME — 500-5   0.124.85 68.1 6724 CPME — 551-0.01 0.31 5.93 66.6 5182 CPME 3-MCH 381-20  0.060 4.83 68.3 (75 vol %) (25 vol %) 5443 CPME 3-MCH 381-20   0.0605.07 52.8 (75 vol %) (25 vol %) 5868 CPME 3-MCH 381-20   0.060 4.97 70.0(75 vol %) (25 vol %) 6551 DIBK — 500-5   0.080 4.78 69.2 6671 DIBK —500-5   0.080 4.94 71.9 6672 DIBK — 551-0.01 0.23 5.50 61.2 5108 DIBK3-MCH 381-20   0.060 4.56 39.4 (75 vol %) (25 vol %) 5382 DIBK 3-MCH381-20   0.060 4.77 45.0 (75 vol %) (25 vol %) 6725 DIBK Cyclo- 381-20  0.047 4.59 50.2 (75 vol %) hexanone (25 vol %) 9355 MAK — 381-20   0.0604.86 65.8 11854 DIBK 2-MCH 381-20   0.036 5.04 (75 vol %) (25 vol %)

TABLE 3 K_(D) data for three test proteins in gel filtration experimentsperformed with prototypes packed in columns Alpha Samplechymotrypsinogen Ribonuclease Lysozyme 5133 0.077 0.224 0.409 5505 0.0560.229 0.418 5595 0.102 0.281 0.457 5892 0.120 0.294 0.472 5928 0.1050.279 0.468 4904 0.059 0.341 0.510 5624 0.072 0.213 0.395 5806 0.1120.293 0.466 6462 0.106 0.257 0.435 6724 0.171 0.330 0.508 5182 0.0810.248 0.425 5443 0.130 0.277 0.462 5868 0.115 0.283 0.461 6551 0.1110.265 0.448 6671 0.099 0.257 0.441 6672 0.153 0.303 0.487 5108 0.0170.130 0.337 5382 0.078 0.258 0.435 6725 0 0.167 0.403 9355 0.101 0.2510.432 11854 0.099 0.259 0.453

The solvents used were also analysed by NMR spectroscopy before andafter emulsification model experiments performed in the absence ofdextran and the emulsifier. The spectra before and after wereessentially identical, showing that no degradation occurred during thereaction conditions used. This was in contrast to an ester solvent,t-butyl acetate, which although being a sterically hindered ester, wascompletely hydrolysed under the strongly alkaline conditions used.

Discussion

The solvents evaluated produce beads that can be used forchromatography, as evidenced e.g. by their performance in the SECanalysis. The measured properties are in the same range as for thereference prototypes, which shows that the new solvents perform well.Due to the different interactions between the solvents and the CABemulsifier, the CAB type and concentration had to be varied in order toget suitable oil phase viscosities. The beads were generally spherical(FIGS. 7-11), but with the solvents 3-MCH and 4-MCH (particularly whenused alone), some inclusions and dimples occurred on the beads.

This written description uses examples to disclose the invention,including the best mode, and also to enable any person skilled in theart to practice the invention, including making and using any devices orsystems and performing any incorporated methods. The patentable scope ofthe invention is defined by the claims, and may include other examplesthat occur to those skilled in the art. Such other examples are intendedto be within the scope of the claims if they have structural elementsthat do not differ from the literal language of the claims, or if theyinclude equivalent structural elements with insubstantial differencesfrom the literal languages of the claims. Any patents or patentapplications mentioned in the text are hereby incorporated by referencein their entireties, as if they were individually incorporated.

1.-20. (canceled)
 21. A polysaccharide bead, prepared by a methodcomprising the steps of: i) providing a water phase comprising anaqueous solution of a polysaccharide and an alkali, wherein the alkaliis present in the water phase at a concentration of 0.1 M to 2 M; ii)providing an oil phase comprising at least one water-immiscible organicsolvent and at least one oil-soluble emulsifier; iii) emulsifying saidwater phase in said oil phase to form a water-in-oil (w/o) emulsion; andiv) inducing solidification of said water phase in said w/o emulsion toform substantially spherical polysaccharide beads, wherein said at leastone organic solvent is an alicyclic ketone or an ether.
 22. Acrosslinked polysaccharide bead, comprising at least 0.1 ppm, such as0.1-100 ppm of a C₆-C₁₀ aliphatic or alicyclic ketone or ether.
 23. Thecrosslinked polysaccharide bead of claim 22, wherein said C₆-C₁₀aliphatic or alicyclic ketone or ether is defined by Formula I, II orIII, such as by Formula II,

wherein: R₁ and R₂ are, independently of each other, C₁-C₅ alkyl groups;R₃ is a C₁-C₅ alkylene group; R₄ is hydrogen or a C₁-C₅ alkyl group; andR₅ and R₆ are, independently of each other, C₁-C₆ alkyl or cycloalkylgroups.
 24. The crosslinked polysaccharide bead of claim 22, whereinsaid C₆-C₁₀ aliphatic or alicyclic ketone or ether is selected from thegroup consisting of 2-methylcyclohexanone, 3-methylcyclohexanone,4-methylcyclohexanone, cyclohexanone, diisobutylketone, methyln-amylketone, methyl isoamyl ketone, methyl isobutyl ketone, cyclopentylmethyl ether and their mixtures.
 25. The bead of claim 21, wherein saidorganic solvent is selected from the group consisting of2-methylcyclohexanone, 3-methylcyclohexanone, 4-methylcyclohexanone andcyclohexanone.
 26. The crosslinked polysaccharide bead of claim 22,having a diameter of 40-125 μm in dry form.
 27. The crosslinkedpolysaccharide bead of claim 22, comprising at least 0.1 mmol/g, or 1-6mmol/g, covalently bonded charged groups, such as carboxymethyl-,sulfopropyl-, diethyl aminoethyl-, and/ordiethyl-(2-hydroxy-propyl)aminoethyl-groups. 28.-29 (canceled)